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Tytuł artykułu

Heat and mass transfer in two-phase gas-droplet turbulent developing flow in a tube

Wybrane pełne teksty z tego czasopisma
Identyfikatory
Warianty tytułu
Języki publikacji
EN
Abstrakty
EN
A computation model is developed, where flow dynamics together with heat and mass transfer in a turbulent two-phase gas-droplet developing tube flow are numerically studied. Turbulent characteristics of the gas phase were calculated using the Nagano-Tagawa LRN k - model. It is shown that, with increasing initial droplet diameter the heat transfer between the duct surface and the vapour-gas mixture becomes much less intense, whereas the wall friction increases only insignificantly. The computed flow-dynamics and heat and mass transfer data are compared with previously reported experimental and numerical results, and a fairly good agreement between the compared data is obtained.
Rocznik
Strony
59--80
Opis fizyczny
Bibliogr. 17 poz.,
Twórcy
autor
  • Kutateladze Institute of Thermophysics, Novosibirsk, Rosja
autor
  • Kutateladze Institute of Thermophysics, Novosibirsk, Rosja
Bibliografia
  • [1] KOIZUMI Y., UEDA T., TANAKA H.: Post dryout heat transfer to R-113 upward flow in a vertical tube, Int. J. Heat Mass Trans., 22(1979), No. 8, 669-678.
  • [2] TRELA M.: An approximate calculation of heat transfer during flow of an air-water mist along heated flat plate, Int. J. Heat Mass Trans., 24(1981), No. 4, 749-755.
  • [3] MASTANAIAH K., GANIC E. N.: Heat transfer in two-component dispersed flow, J. Heat Transfer, Trans. of ASME, 103(1981), No. 2, 300-306.
  • [4] SIKALO S., DELALIĆ N., GANIĆ E. N.: Hydrodynamics and heat transfer investigation of air-water dispersed flow, Int. J. Experimental Thermal and Fluid Sci., 25(2002), No. 7, 511-521.
  • [5] TEREKHOV V. I., PAKHOMOV M. A., CHICHINDAEV A. V.: Heat and mass transfer in a two-component turbulent developed gas-vapour-droplet flow, J. Eng. Phys. and Thermophysics, 74(2001), No. 2, 331-338.
  • [6] TEREKHOV V. I., PAKHOMOV M. A., CHICHINDAEV A. V.: Effect of evaporation of liquid droplets on the distribution of parameters in a two-species laminar flow, J. Appl. Mech. and Tech. Physics, 41(2000), No. 6, 1020-1028.
  • [7] TEREKHOV V. I., PAKHOMOV M. A.: Numerical study of heat transfer in a laminar mist flow over a isothermal flat plate, Int. J. Heat Mass Transfer, 45(2002), No. 10, 2077-2085.
  • [8] DEISSLER R. G.: Analysis of turbulent heat transfer, mass transfer, and friction in smooth tubes at high Prandtl and Schmidt numbers, NACA TR 1210, Washington, D.C., USA, 1955.
  • [9] NAGANO Y., TAGAWA M.: An improved (k - ε) model for boundary layer flow, J. Fluids Eng., Trans. of ASME, 109 (1990), No. 1, 33-39.
  • [10] CROWE C. T., SOMMERFELD M., TSUJI Y.: Multiphase flow with droplets and particles, Boca Raton, CRC Press 1998.
  • [11] KUTATELADZE S. S., LEONT'EV A. I.: Heat and mass transfer, and friction in turbulent boundary layer, Washington, Hemisphere 1989.
  • [12] YUEN M. C., CHEN L. W. Heat transfer measurements of evaporating liquid droplets, Int. J. Heat Mass Trans., 21(1979), No. 5, 537-542.
  • [13] GUSEV I. N., GUSEVA E. I, ZAICHIK L. I.: Deposition of particle on channel walls in a turbulent flow, J. Eng. Phys. and Thermophysics, 59(1990), No. 5, 735-742.
  • [14] ANDERSON J.D., JR., ET AL.: Introduction to computational fluid dynamics, Ed. J. F. Wendt. Berlin, Springer 1992.
  • [15] EGGELS J. G. M., UNGER F., WEISS M. H., ET AL.: Fully developed pipe flow: a comparison between direct numerical simulation and experiment, J. Fluid Mechanics, 268 (1994), 175-209.
  • [16] LAUFER J.: The structure of turbulence in fully developed pipe flow, NACA TR 1174, Washington, D.C., USA, 1954.
  • [17] RANE A. G., YAO S.-CH.: Convective heat transfer to turbulent droplet flow in circular tubes, J. Heat Transfer, Trans. of ASME, 103(1981), No. 4, 679-684.
Typ dokumentu
Bibliografia
Identyfikator YADDA
bwmeta1.element.baztech-article-BGPK-0379-2503
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